Method and device for separating formaldehyde and refining PODE2
A technology of PODE2 and formaldehyde, which is applied in the field of chemical engineering, can solve the problems of severe equipment corrosion, high energy consumption for separation, and difficult formaldehyde separation, and achieve the effect of energy saving
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Embodiment 1
[0036] Methanol, formaldehyde, water and PODE 2 The raw material of the mixture enters the first rectifying tower, and the operating pressure of the first rectifying tower is 80KPa, adopts figure 1 Feed in the same way, introduce make-up water in the middle of the first rectification tower, the mass ratio of make-up water to raw material is 0.3:1; the production fluid from the top of the first rectification tower enters the molecular sieve dehydration unit to remove water, and the molecular sieve is 3A molecular sieve The material that has dehydrated enters the second rectifying tower, and the operating pressure of the second rectifying tower is 80KPa;
[0037] After the above process, the top of the first rectification tower basically does not contain formaldehyde, and the mass fraction of formaldehyde in the formaldehyde-containing aqueous solution in the tower kettle is 42%. After cooling, there is no problem of formaldehyde polymerization blocking the pipeline, and the POD...
Embodiment 2
[0039] Methanol, formaldehyde, water and PODE 2 The raw material of the mixture enters the first rectifying tower, and the operating pressure of the first rectifying tower is 100KPa, adopts figure 1 Feed in the same way, introduce make-up water in the middle of the first rectification tower, the mass ratio of make-up water to raw material is 0.5:1; the production fluid from the top of the first rectification tower enters the membrane dehydration unit to remove water; The material enters the second rectifying tower, and the operating pressure of the second rectifying tower is 100KPa;
[0040] After the above process, the top of the first rectification tower basically does not contain formaldehyde, and the mass fraction of formaldehyde in the formaldehyde-containing aqueous solution in the tower kettle is 37%. 2 The quality fraction is greater than 99%.
Embodiment 3
[0042] Methanol, formaldehyde, water and PODE 2 The raw material of the mixture enters the first rectifying tower, and the operating pressure of the first rectifying tower is 120KPa, adopts figure 2 Feed in the same way, introduce make-up water in the middle of the first rectification tower, the mass ratio of make-up water to raw material is 1:1; the production liquid from the top of the first rectification tower enters the adsorption dehydration unit to remove water; The material enters the second rectifying tower, and the operating pressure of the second rectifying tower is 120KPa;
[0043] After the above process, the top of the first rectifying tower basically does not contain formaldehyde, and the mass fraction of formaldehyde in the formaldehyde-containing aqueous solution in the tower kettle is 20%, and there is no problem of formaldehyde polymerization blocking the pipeline after cooling, and the PODE 2 The quality fraction is greater than 99%.
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